CN1523207A - Nox catalyst regeneration method for nox purifying system and nox purifying system - Google Patents
Nox catalyst regeneration method for nox purifying system and nox purifying system Download PDFInfo
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- CN1523207A CN1523207A CNA200410005580XA CN200410005580A CN1523207A CN 1523207 A CN1523207 A CN 1523207A CN A200410005580X A CNA200410005580X A CN A200410005580XA CN 200410005580 A CN200410005580 A CN 200410005580A CN 1523207 A CN1523207 A CN 1523207A
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02D—CONTROLLING COMBUSTION ENGINES
- F02D41/00—Electrical control of supply of combustible mixture or its constituents
- F02D41/02—Circuit arrangements for generating control signals
- F02D41/021—Introducing corrections for particular conditions exterior to the engine
- F02D41/0235—Introducing corrections for particular conditions exterior to the engine in relation with the state of the exhaust gas treating apparatus
- F02D41/027—Introducing corrections for particular conditions exterior to the engine in relation with the state of the exhaust gas treating apparatus to purge or regenerate the exhaust gas treating apparatus
- F02D41/0275—Introducing corrections for particular conditions exterior to the engine in relation with the state of the exhaust gas treating apparatus to purge or regenerate the exhaust gas treating apparatus the exhaust gas treating apparatus being a NOx trap or adsorbent
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
- B01D53/9495—Controlling the catalytic process
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02D—CONTROLLING COMBUSTION ENGINES
- F02D2200/00—Input parameters for engine control
- F02D2200/02—Input parameters for engine control the parameters being related to the engine
- F02D2200/08—Exhaust gas treatment apparatus parameters
- F02D2200/0802—Temperature of the exhaust gas treatment apparatus
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- Combustion & Propulsion (AREA)
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- General Chemical & Material Sciences (AREA)
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- Chemical Kinetics & Catalysis (AREA)
- Exhaust Gas After Treatment (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Provided is a method for regenerating the NOx catalyst of an NOx purifying system and an NOx purifying system enabling the suppression of discharge of NOx into the atmosphere when exhaust gas is temporarily brought into a rich condition to regenerate a catalyst to recover the NOx purifying ability of a direct reduction type NOx catalyst situated in the exhaust passage of an engine and capable of reliably recovering NOx purifying performance. In the method for regenerating the NOx catalyst in the NOx purifying system where the direct reduction type NOx catalyst to directly decompose NOx at a lean time and regenerate it at a rich time is situated in an exhaust passage, the control of a rich condition is prohibited when a temperature detected by a catalyst temperature detecting means is in a given temperature range.
Description
Technical field
The present invention relates to a kind of NOx catalyst recovery process and NOx system system of NOx system system, it is with direct reduced form NOx catalyzer the NOx (nitrogen oxide) in the waste gas of internal-combustion engine discharge to be purified.
Background technique
Relevant from automobile internal-combustion engine or the waste gas of the formula of arrangement internal-combustion engine etc. catalyst type waste gas cleaning plant that the NOx reduction is removed, all research and motion were arranged, particularly for the waste gas with automobile etc. purifies, and use NOx absorbing and reducing type catalyzer or three-way catalyst etc.
In the waste gas cleaning plant of the internal-combustion engine in the exhaust passageway that this NOx absorbing and reducing type catalyzer is configured in internal-combustion engine, carry out regenerative operation, promptly, in the air fuel ratio of the waste gas that flows into when being rare, make NOx absorbing and reducing type catalyzer absorption of N Ox, when the NOx absorptivity when saturated, the oxygen concentration of exhaust gases of inflow is reduced, become chemically correct fuel or dense proportions of ingredients state by the air fuel ratio that makes waste gas, the NOx of absorption is discharged, so that the NOx absorptivity recovers, and by and the noble metal catalyst established make the NOx reduction that is discharged from.
In this NOx absorbing and reducing type catalyzer, be carried with platinum noble metal catalysts such as (Pt) and barium NOx absorbing agents such as alkali earths such as (Ba) on the catalyst carrier, under hyperoxia concentration atmosphere, by the effect of catalyzer such as platinum, the NO in the waste gas is oxidized into NO
2, with NO
3-form spreads in catalyzer, and is absorbed with the form of nitrate.
And, when air fuel ratio becomes dense proportions of ingredients, when oxygen concentration reduces, makes NO
3 -With NO
2Form be discharged from, by be included in the waste gas not the combustion HC, CO or H
2Deng reducing agent, accept catalyst actions such as platinum, and with NO
2Be reduced into N
2Just can stop NOx to be discharged in the atmosphere by this reduction.
There is a problem in this NOx absorbing and reducing type catalyzer, and great changes will take place along with the temperature of NOx absorbing agent is understood for the amount of the NOx that can absorb, thereby manage according to exhaust gas temperature, changes the soak time of NOx, to set only NOx soak time etc.
(for example, referring to Patent Document 1)
On the other hand, catalyzer different with this NOx absorbing and reducing type catalyzer in addition, that make the direct reduction of NOx (below, be called direct reduced form NOx catalyzer).This direct reduced form NOx catalyzer is that carriers such as zeolite beta are carried with rhodium (Rh) or the palladium metals such as (Pd) as the catalyzer composition.And, mix cerium (Ce) to alleviate the burning effect, and help to keep the NOx reducing capacity, or three-way catalyst is set with the accelerating oxidation reduction reaction in lower floor, particularly promote the reduction reaction of the NOx under the dense proportions of ingredients state, perhaps in order to improve the purification ratio of NOx, and in carrier, add iron (Fe) etc.
The advantage that this direct reduced form NOx catalyzer has is that the problem of being poisoned by sulphur is seldom arranged, and is in the atmosphere of the such hyperoxia concentration of the waste gas of rare proportions of ingredients state in the air fuel ratio of internal-combustion engines such as diesel engine, and NOx directly is reduced into N
2, but when carrying out this reduction, because O
2Be adsorbed on the metal as the activity of such catalysts material, thereby reducing property is worsened.
Therefore,, need make oxygen concentration in the waste gas roughly become the low state of O%, make the regeneration of activity of such catalysts material and activate for the air fuel ratio that makes waste gas becomes chemically correct fuel or dense proportions of ingredients state.In addition, the regeneration of this catalyzer is compared with other catalyzer, even also can carry out rapidly in low temperature (for example more than 200 ℃).
Therefore, in the Nox cleaning system in the exhaust passageway that will this direct reduced form NOx catalyzer be arranged on motor, in order to give full play to the purifying property of NOx, in engine operation, must carry out suitable conversion to the dense proportions of ingredients condition control that the rare proportions of ingredients condition in the common running is controlled and catalyst regeneration is used.
Patent documentation 1 is opened flat 7-102954 communique (the 2nd page, the 3rd page) for the open communique spy of Japan Patent.
But, in this direct reduced form NOx catalyzer, even carry out dense proportions of ingredients condition control, enter at catalyst temperature under the occasion of high-temperature area, when carrying out the control of dense proportions of ingredients condition for the regeneration of catalyzer, the NOx amount that is discharged in the atmosphere is increased, and owing to can not make catalyst regeneration, thereby purifying property can not recover, and the problem that causes that fuel cost worsens is arranged.
Though promptly this direct reduced form NOx catalyzer is different with NOx absorbing and reducing type catalyzer, do not carry out NOx adsorption by chemical bond, but it is the phenomenon along with the physical property NOx adsorption, makes the relation of the extent of adsorption of this NOx and catalyst temperature become as shown in Figure 3 relation.Even therefore be judged to be under dense proportions of ingredients condition, when catalyst temperature enters high-temperature area, the NOx extent of adsorption is reduced, that of minimizing part NOx is discharged from, and the NOx discharge capacity is increased.
Fig. 4 is that expression is turned round with the dense proportions of ingredients condition of chemically correct fuel, and the catalyst outlet NOx concentration the when exhaust gas temperature of catalyst outlet is risen.As seen from Figure 4, although a certain amount of Nox is supplied to the NOx catalyzer, the amount of catalyst outlet NOx is that the rising with the catalyst outlet exhaust gas temperature changes accordingly, when the catalyst outlet exhaust gas temperature raises, the NOx amount that flow into from inlet side more than the NOx amount of direct reduced form NOx catalyzer is discharged from catalyst outlet, particularly just significantly increases in time more than 420 °.
The content of invention
The present invention makes for the problem that solves above-mentioned prior art existence, its objective is NOx catalyst recovery process and NOx system system that a kind of NOx system system is provided, it is the catalyst regeneration that is used to make the NOx purification capacity recovery that is arranged on the direct reduced form NOx catalyzer on the engine exhaust path, when making waste gas become dense proportions of ingredients condition temporarily, differentiate whether transfer to dense proportions of ingredients condition control according to the temperature that detects by catalyst temperature feeler mechanism, and only when the temperature that is detected by catalyst temperature feeler mechanism is in certain temperature range, just shift to dense proportions of ingredients condition control, thus, can control the discharge of NOx in atmosphere, purifying property is recovered.
The NOx catalyst recovery process of the NOx system system of the present invention of making in order to achieve the above object, it is to be provided with direct reduced form NOx catalyzer in exhaust passageway, when rare proportions of ingredients condition, NOx is directly decomposed, and when dense proportions of ingredients condition, be reproduced, it is characterized in that, the temperature that is detected by catalyst temperature feeler mechanism is forbidden dense proportions of ingredients condition control in predetermined temperature range the time.
And, be used to implement the NOx system system of the NOx catalyst recovery process of above-mentioned NOx system system, be in exhaust passageway, to be provided with direct reduced form NOx catalyzer, when rare proportions of ingredients condition, NOx is directly decomposed, and when dense proportions of ingredients condition, be reproduced, it is characterized in that having catalyst temperature feeler mechanism; And be provided with control gear, when the temperature that is detected by catalyst temperature feeler mechanism is in predetermined temperature range, forbid the control of dense proportions of ingredients condition.
This direct reduced form NOx catalyzer, its formation are that carriers such as zeolite beta are carried with rhodium (Rh) and the palladium particulate metal such as (Pd) as the catalyzer composition.And the dense proportions of ingredients condition that is used for catalyst regeneration is controlled, can with the gettering quantity control of suction throttling valve etc., and back fuel injection control of spraying etc. or EGR control etc. implemented, above-mentioned predetermined temperature range is meant the temperature range of being tried to achieve by methods such as experiments, try to achieve from predefined numerical value or nominal data (マ Star プ デ one ) etc., than the predetermined also high high-temperature area of decision content such in 400 ℃～500 ℃ scope.
The catalyst temperature of being determined by catalyst temperature feeler mechanism or the detection of exhaust gas temperature can be considered to carry out method for measuring in catalyzer or the exhaust passageway or the catalyst temperature figure that set through verification in advance by engine revolution and accelerator pedal aperture, reference or exhaust gas temperature figure and the method calculated etc. with shown in Figure 2 temperature transducer is configured in.
And, NOx catalyst recovery process and NOx system system according to this NOx system system, owing to be the NOx system system of purification that direct reduced form NOx catalyzer is used for the NOx of waste gas, when dense proportions of ingredients condition is controlled, the catalyst temperature scope that can avoid making the NOx concentration of catalyst outlet to increase, and carry out dense proportions of ingredients condition control, thereby can prevent that NOx from discharging in atmosphere, can purify the NOx in the waste gas efficiently simultaneously.And, because under dense proportions of ingredients condition, can positively make direct reduced form NOx catalyst regeneration, thereby can prevent the deterioration of fuel cost.
The simple declaration of accompanying drawing
Fig. 1 is the figure of the engine system that is provided with waste gas cleaning system of expression embodiments of the present invention, and this waste gas cleaning system has direct reduced form NOx catalyzer.
Fig. 2 is the control flow chart of expression embodiment of the present invention.
The schematic representation of the characteristic of the direct reduced form NOx catalyzer when Fig. 3 is expression maintenance dense proportions of ingredients (リ Star チ) condition.
Fig. 4 is the schematic representation of the relation of expression catalyst temperature of direct reduced form NOx catalyzer and NOx extent of adsorption.
The embodiment of invention
Below, with reference to accompanying drawing NOx catalyst recovery process and the NOx system system that NOx system of the present invention is united is described.
As shown in Figure 1, in this NOx system system 10, in the air suction way (sucking pipe) 2 of motor 1, compressor 31a, interstage cooler 22 and the intake-air throttle valve (suction throttling valve) 23 of suction air quantity sensor (a large amount of airflow sensor) 21, turbosupercharger 31 is being set; The turbine 31b of turbosupercharger 31 and direct reduced form NOx catalyzer 32 are being set in exhaust passageway (outlet pipe) 3, and at EGR path (EGR pipe: the exhaust cycle path) cooler for recycled exhaust gas 41 and EGR valve 42 are being set in 4.
Directly also setting the temperature transducer 71 that is used to detect catalyst temperature on the reduced form NOx catalyzer 32 as catalyst temperature feeler mechanism.Use under the occasion of exhaust gas temperature in the alternative catalysts temperature, temperature transducer 71 is provided near the inlet of direct reduced form NOx catalyzer 32 or near the outlet.
In fuel injection system, be provided with and be used for fuel F, the device that parameter such as the control gear 60 that is called ECU (engine control assembly), aperture Acc, engine revolution Ns that it is the input accelerator pedal, crankangle CA also is being set and motor is controlled from the petrolift 51 of the fuel chambers 54 of fuel bath (figure do not have expression) supply engine, rail (コ モ Application レ one Le) 52 and Fuelinjection nozzle (oil sprayer) 53 altogether.
Directly the structure of reduced form NOx catalyzer 32 is that carriers such as zeolite beta are carried with rhodium (Rh) or palladium particulate metal such as (Pd).In addition, such situation is arranged also, promptly, mix cerium (Ce), help to alleviate burning effect, and the NOx reducing capacity that keeps; Perhaps the three-way catalyst with platinum etc. is set, with the accelerating oxidation reduction reaction, particularly promote the reduction reaction of the NOx under the dense proportions of ingredients state in lower floor; And iron (Fe) etc. is added carrier for the purification ratio that improves NOx.
The waste gas that the air fuel ratio as internal-combustion engines such as diesel engines is in rare proportions of ingredients (リ one Application) state, in the high atmosphere of oxygen concentration, this direct reduced form NOx catalyzer 32 is contacted with NOx and make NOx directly be reduced into N
2, simultaneously with O
2Be adsorbed on the activity of such catalysts material, reducing capacity is reduced.This reducing capacity be can be when making air fuel ratio be in chemically correct fuel or dense proportions of ingredients like that, make oxygen concentration in the waste gas roughly become 0% reducing atmosphere to regenerate.
And the catalyst regeneration of NOx system system is that basis control flow as shown in Figure 2 carries out.This control flow is the flow process of implementing concurrently with the control flow of motor, come into effect simultaneously with the motor entry into service, finish with the running of motor control flow to be stopped, when promptly stopping working control flow is stopped with engine ignition switch key OFF.
And, when this control flow begins, just enter rare mixing condition control.At step S11, input engine revolution Ne and fuel injection amount Q; At step S12, by this engine revolution Ne and fuel injection amount Q, calculate rare proportions of ingredients set time tls with reference to rare proportions of ingredients set time figure.
Then, at step S13, carry out one period scheduled time the rare proportions of ingredients condition control of (with the relevant time in the time lag of control); Carry out the judgement that rare proportions of ingredients condition control finishes at step S14.
In above-mentioned steps S13, the NOx in the waste gas contacts with the active substance of direct reduced form NOx catalyzer 32, and NOx is reduced into N
2Since when carrying out this reduction, O
2Adsorbed by active substance, thereby reducing capacity just reduces gradually.
Then, judge by the end that rare proportions of ingredients condition of step S14 is controlled, surpass rare proportions of ingredients set time tls, promptly be judged to be rare proportions of ingredients condition control time when not finishing being judged to be rare proportions of ingredients cumulative time tl, revert to step 13, carry out rare proportions of ingredients condition control repeatedly, and surpass set time tls, promptly be judged to be rare proportions of ingredients condition control when finishing being judged to be rare proportions of ingredients cumulative time tl, enter into step S15.
At step S15, enter catalyst temperature (or exhaust gas temperature) Te, whether be lower than predetermined setting temperature Te0 at step S16, judgement catalyst temperature Te.At step S16, because under the high occasion of the predetermined setting temperature Te0 of catalyst temperature Te ratio, in case transfer to dense proportions of ingredients condition control, just produce the discharge of NOx, thereby turn back to step S13, carry out rare proportions of ingredients condition control repeatedly, be lower than predetermined setting temperature Te0 up to catalyst temperature Te.In addition, have under the occasion of the direct reduced form NOx catalyzer of characteristic as shown in Figure 3, this predetermined setting temperature Te0 is set at for example temperature in 400 ℃～500 ℃ scopes.
And in step 16, under the low occasion of the predetermined setting temperature Te0 of catalyst temperature Te ratio, even carry out dense proportions of ingredients condition control, owing to do not produce the discharge of NOx yet, thereby enter into step S17, transfer to dense proportions of ingredients condition control program.
At step S17, input engine revolution Ne and fuel injection amount Q at next procedure S18, according to engine revolution Ne and fuel injection amount Q, calculate dense proportions of ingredients set time trs with reference to dense proportions of ingredients set time figure.
Then, at next procedure S19, in one section preset time (with the relevant time in the time lag of control), carry out dense proportions of ingredients condition control.In this dense proportions of ingredients condition control, carry out the dense proportions of ingredients condition control of the air-breathing throttling control of predefined intake-air throttle valve 23 or secondary injection etc. accordingly with engine revolution Ne and fuel injection amount Q, make the oxygen concentration in the waste gas be roughly 0%, make waste gas become dense proportions of ingredients state, can make the active substance activation thus, make catalyst regeneration.
Whether the step S20 after step S19 surpasses dense proportions of ingredients set time trs, judges whether dense proportions of ingredients condition control finishes according to dense proportions of ingredients cumulative time tr.
Judgement according to above-mentioned steps S20, under the occasion that dense proportions of ingredients condition control does not have to finish, carry out the dense proportions of ingredients condition control of step S19 repeatedly, last till that dense proportions of ingredients condition control finishes, and, turn back to step S11 according to the judgement of step S20, under the occasion that dense proportions of ingredients condition control finishes.
Carry out above step S11～step S20 repeatedly, in the process of implementation, when the engine ignition switch key of generation step S21 inserts OFF, after step S22 controls the end operation, for example under the occasion that in the process of rare proportions of ingredients condition control or the control of dense proportions of ingredients condition, stops, just stop after rare proportions of ingredients cumulative time tl or dense proportions of ingredients cumulative time tr stored, so that when beginning this control flow next time, can be with the initial value of rare proportions of ingredients cumulative time tl or the dense proportions of ingredients cumulative time tr value when stopping.
According to the above-mentioned NOx system system and the control of catalyst regeneration thereof, in dense proportions of ingredients condition control, because the catalyst temperature scope that can avoid making the NOx concentration of catalyst outlet to increase, control and carry out dense proportions of ingredients condition, thereby can prevent that NOx from discharging in atmosphere, can purify the NOx in the waste gas efficiently, and can prevent the deterioration of fuel cost.
Effect of the present invention.
NOx catalyst recovery process and NOx according to NOx system system of the present invention are clean The change system, this NOx system system is used for waste gas with direct-reduction type NOx catalyst The purification of NOx when dense mixing ratio condition control, owing to can avoid making catalyst outlet The catalyst temperature scope that increases of NOx concentration and carry out dense mixing ratio condition control, thereby Can prevent that NOx from discharging in atmosphere, can purify the NOx in the waste gas efficiently simultaneously. Because under dense mixing ratio condition, can positively make direct-reduction type NOx catalyst regeneration, Thereby can prevent the deterioration of fuel cost.
Claims (2)
1, the NOx catalyst recovery process of NOx system system, it is to be provided with direct reduced form NOx catalyzer in exhaust passageway, this direct reduced form NOx catalyzer directly decomposes NOx when rare proportions of ingredients, and when dense proportions of ingredients, be reproduced, it is characterized in that, the temperature that is detected by catalyst temperature feeler mechanism is in predetermined temperature range the time, forbids dense proportions of ingredients condition control.
2., NOx system system, it is to be provided with direct reduced form NOx catalyzer in exhaust passageway, and this direct reduced form NOx catalyzer directly decomposes NOx when rare proportions of ingredients, and is reproduced when dense proportions of ingredients condition, it is characterized in that having catalyst temperature feeler mechanism; And have control gear, when the temperature that is detected by catalyst temperature feeler mechanism is in the predetermined temperature range, forbid the control of dense proportions of ingredients condition.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2003041478A JP4168781B2 (en) | 2003-02-19 | 2003-02-19 | NOx catalyst regeneration method for NOx purification system and NOx purification system |
| JP2003041478 | 2003-02-19 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1523207A true CN1523207A (en) | 2004-08-25 |
| CN100343492C CN100343492C (en) | 2007-10-17 |
Family
ID=32732946
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB200410005580XA Expired - Fee Related CN100343492C (en) | 2003-02-19 | 2004-02-18 | Nox catalyst regeneration method for nox purifying system and nox purifying system |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US7168242B2 (en) |
| EP (1) | EP1449575B1 (en) |
| JP (1) | JP4168781B2 (en) |
| CN (1) | CN100343492C (en) |
| DE (1) | DE602004015653D1 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102083532A (en) * | 2009-07-17 | 2011-06-01 | 克拉基斯技术控股公司 | Method for removing a catalyst inhibitor from a substrate |
| CN101874964B (en) * | 2009-12-11 | 2012-05-09 | 北京科技大学 | Low temperature storage and reduction method for purifying oxynitrides |
| CN102563589A (en) * | 2010-10-29 | 2012-07-11 | 通用电气公司 | Systems, methods, and apparatus for regenerating a catalytic material |
| CN107208518A (en) * | 2015-01-22 | 2017-09-26 | 五十铃自动车株式会社 | Emission control system and catalyst recovery process |
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| JP3912294B2 (en) * | 2003-02-19 | 2007-05-09 | トヨタ自動車株式会社 | Exhaust gas purification method and exhaust gas purification apparatus for internal combustion engine |
| FR2865773B1 (en) * | 2004-02-03 | 2006-06-30 | Peugeot Citroen Automobiles Sa | SYSTEM FOR AIDING THE REGENERATION OF INTEGRATED EMISSION MEANS IN AN EXHAUST LINE OF A THERMAL ENGINE |
| US7441403B2 (en) * | 2004-12-20 | 2008-10-28 | Detroit Diesel Corporation | Method and system for determining temperature set points in systems having particulate filters with regeneration capabilities |
| US7210286B2 (en) * | 2004-12-20 | 2007-05-01 | Detroit Diesel Corporation | Method and system for controlling fuel included within exhaust gases to facilitate regeneration of a particulate filter |
| US7461504B2 (en) * | 2004-12-21 | 2008-12-09 | Detroit Diesel Corporation | Method and system for controlling temperatures of exhaust gases emitted from internal combustion engine to facilitate regeneration of a particulate filter |
| US20060130465A1 (en) * | 2004-12-22 | 2006-06-22 | Detroit Diesel Corporation | Method and system for controlling exhaust gases emitted from an internal combustion engine |
| US7434388B2 (en) | 2004-12-22 | 2008-10-14 | Detroit Diesel Corporation | Method and system for regeneration of a particulate filter |
| US7076945B2 (en) | 2004-12-22 | 2006-07-18 | Detroit Diesel Corporation | Method and system for controlling temperatures of exhaust gases emitted from an internal combustion engine to facilitate regeneration of a particulate filter |
| EP2039995A1 (en) * | 2006-07-04 | 2009-03-25 | Miura Co., Ltd. | Method of combustion and combustion apparatus |
| JP6135198B2 (en) * | 2013-03-07 | 2017-05-31 | いすゞ自動車株式会社 | Control method of exhaust gas aftertreatment device |
| US9255537B2 (en) * | 2013-03-15 | 2016-02-09 | GM Global Technology Operations LLC | Rejuvenation control of palladium-only diesel oxidation catalyst |
| US10221792B2 (en) | 2013-08-15 | 2019-03-05 | Ford Global Technologies, Llc | Two-stage catalyst regeneration |
| CN104295344A (en) * | 2014-09-12 | 2015-01-21 | 苏州博菡环保科技有限公司 | Automobile exhaust purifier |
| JP6235538B2 (en) * | 2015-07-21 | 2017-11-22 | 本田技研工業株式会社 | Exhaust gas purification device for internal combustion engine |
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| JP2783074B2 (en) * | 1991-10-29 | 1998-08-06 | トヨタ自動車株式会社 | Exhaust gas purification device for internal combustion engine |
| JP3157061B2 (en) * | 1993-04-26 | 2001-04-16 | 株式会社日立製作所 | Catalyst deterioration diagnosis system |
| JP2888109B2 (en) | 1993-09-30 | 1999-05-10 | トヨタ自動車株式会社 | Exhaust gas purification device for internal combustion engine |
| WO1997016632A1 (en) * | 1995-10-30 | 1997-05-09 | Toyota Jidosha Kabushiki Kaisha | Exhaust emission control apparatus for internal combustion engine |
| US5704339A (en) * | 1996-04-26 | 1998-01-06 | Ford Global Technologies, Inc. | method and apparatus for improving vehicle fuel economy |
| EP1164268B1 (en) * | 1997-04-09 | 2006-05-24 | Emitec Gesellschaft für Emissionstechnologie mbH | Arrangement for monitoring a NOx-trap |
| DE19753718C1 (en) * | 1997-12-04 | 1999-07-08 | Daimler Chrysler Ag | Method for operating a diesel engine |
| DE19852240A1 (en) * | 1998-11-12 | 2000-05-18 | Volkswagen Ag | Monitoring method for NOx storage catalytic converters and exhaust gas purification device for carrying out this method |
| CN100349052C (en) * | 1998-11-27 | 2007-11-14 | 夏普株式会社 | Illuminator, lighting component, head light and LCD |
| EP1065351B1 (en) * | 1999-07-02 | 2004-03-03 | Mitsubishi Jidosha Kogyo Kabushiki Kaisha | Exhaust gas purifying apparatus of internal combustion engine |
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2003
- 2003-02-19 JP JP2003041478A patent/JP4168781B2/en not_active Expired - Fee Related
-
2004
- 2004-02-02 EP EP04100355A patent/EP1449575B1/en not_active Expired - Lifetime
- 2004-02-02 DE DE602004015653T patent/DE602004015653D1/en not_active Expired - Lifetime
- 2004-02-10 US US10/774,490 patent/US7168242B2/en not_active Expired - Lifetime
- 2004-02-18 CN CNB200410005580XA patent/CN100343492C/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102083532A (en) * | 2009-07-17 | 2011-06-01 | 克拉基斯技术控股公司 | Method for removing a catalyst inhibitor from a substrate |
| CN101874964B (en) * | 2009-12-11 | 2012-05-09 | 北京科技大学 | Low temperature storage and reduction method for purifying oxynitrides |
| CN102563589A (en) * | 2010-10-29 | 2012-07-11 | 通用电气公司 | Systems, methods, and apparatus for regenerating a catalytic material |
| US9062569B2 (en) | 2010-10-29 | 2015-06-23 | General Electric Company | Systems, methods, and apparatus for regenerating a catalytic material |
| CN107208518A (en) * | 2015-01-22 | 2017-09-26 | 五十铃自动车株式会社 | Emission control system and catalyst recovery process |
| US10480436B2 (en) | 2015-01-22 | 2019-11-19 | Isuzu Motors Limited | Exhaust purification system and catalyst regeneration method |
| CN107208518B (en) * | 2015-01-22 | 2020-04-03 | 五十铃自动车株式会社 | Exhaust gas purification system and catalyst regeneration method |
Also Published As
| Publication number | Publication date |
|---|---|
| DE602004015653D1 (en) | 2008-09-25 |
| US7168242B2 (en) | 2007-01-30 |
| US20040159097A1 (en) | 2004-08-19 |
| JP4168781B2 (en) | 2008-10-22 |
| EP1449575B1 (en) | 2008-08-13 |
| JP2004251177A (en) | 2004-09-09 |
| EP1449575A1 (en) | 2004-08-25 |
| CN100343492C (en) | 2007-10-17 |
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